CN206463797U - A kind of membrane component of the simplification water-purifying process with a variety of functions - Google Patents
A kind of membrane component of the simplification water-purifying process with a variety of functions Download PDFInfo
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- CN206463797U CN206463797U CN201720049882.XU CN201720049882U CN206463797U CN 206463797 U CN206463797 U CN 206463797U CN 201720049882 U CN201720049882 U CN 201720049882U CN 206463797 U CN206463797 U CN 206463797U
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Abstract
The utility model is related to a kind of membrane component of the simplification water-purifying process with a variety of functions, including diaphragm, production water flow passage cloth, water inlet flow channel cloth and central tube, production water flow passage cloth, the diaphragm folded, the water inlet flow channel cloth being clipped in folding diaphragm are sequentially stacked together volume according to this on central tube, water inlet flow channel cloth and diaphragm composition intake tunnel, composition production aquaporin after water flow passage cloth and diaphragm bonding is produced, production water is collected by central tube.Wherein described water inlet flow channel cloth and/or described production water flow passage cloth by the direct machine-shaping of sorbing material or load sorbing material thereon or by modified grafting method with adsorption function.Wherein described diaphragm selectively passes through diaphragm including micro-filtration, ultrafiltration, nanofiltration and counter-infiltration, and homogeneous diaphragm load or grafting sorbing material in retention layer, heterogeneous diaphragm load or are grafted sorbing material in supporting layer.The utility model, which can provide a kind of membrane component with a variety of functions, can simplify water-purifying process, and purifier cost can be reduced therewith, reduce water purification cost.
Description
Technical field
The application is related to water treatment field, and in particular to a kind of membrane component of the simplification water-purifying process with a variety of functions.
Background technology
Recently as the continuous exposure of water contamination accident, safe drinking water is increasingly valued by people, various therewith
The embrane method purification techniques such as ultrafiltration, nanofiltration, counter-infiltration is widely used in water-purifying process, most of water purification products of in the market
Using PP (PP cottons)+UDF (granular activated carbon)+CTO (sintering activity charcoal)+NF/RO (nanofiltration/counter-infiltration)+UDF (seed activities
Charcoal) technique, wherein PP cotton filter cores are substantially carried out coarse filtration, preposition activated carbon filtration core primary attachment partial organic substances and such as chlorine residue
Oxidizing substance, plays a part of protection nanofiltration/counter-infiltration filter core, and nanofiltration/counter-infiltration filter core is the core component of whole technique,
Most pollutants are all retained by it, and post active carbon filter core primarily serves further absorption residuals, are improved mouthfeel and are made
With.This multistage filtering water-purifying process needs multiple filter cores to be used in series, and structure is numerous and diverse, and purifier product price is higher, no
Beneficial to promoting the use of for water purification product.
It is main by differential permeability diaphragm, water inlet flow channel cloth, production water flow passage as the wound membrane element of water-purifying process core
Cloth and central tube composition, wherein only differential permeability diaphragm filtration, 1/ of its proportion less than membrane component entirety
3, remainder only supports guide functions.The effect of membrane component is single, low space utilization.
Utility model content
In view of this, the utility model provides a kind of membrane component of the simplification water-purifying process with a variety of functions, it is intended that no
Increase in the case of membrane component volume, increase membrane component function, simplify water-purifying process reduction water purification cost.
The technical solution adopted in the utility model is specially:
A kind of membrane component of the simplification water-purifying process with a variety of functions, including diaphragm, production water flow passage cloth, water inlet flow channel cloth
And central tube, production water flow passage cloth, the diaphragm folded, the water inlet flow channel cloth being clipped in folding diaphragm are sequentially stacked together according to this
Volume is on central tube, water inlet flow channel cloth and diaphragm composition intake tunnel, composition production aquaporin after production water flow passage cloth and diaphragm bonding,
Production water is collected by central tube, and the central tube is made up of water inlet end pipe, collector pipe and production water end (W.E.) pipe, is had in the water inlet end pipe
Water inlet dividing plate, diaphragm and production water flow passage cloth both sides vertical with central tube and parallel with central tube and remote central tube are all used seal on one side
Adhesive edge.
Wherein described water inlet flow channel cloth and/or described production water flow passage cloth by the direct machine-shaping of sorbing material or
Sorbing material is loaded thereon or by modified grafting method with adsorption function.
Wherein described diaphragm selectively passes through diaphragm including micro-filtration, ultrafiltration, nanofiltration and counter-infiltration, and homogeneous diaphragm is in retention
Load or grafting sorbing material in layer, heterogeneous diaphragm load or are grafted sorbing material in supporting layer.
Wherein described water inlet end pipe and production water end (W.E.) pipe are waterproof dense material.
Wherein described collector pipe is made up of the sorbing material with sterilizing function and with a large amount of micropore aquaporins.
Wherein described production water end (W.E.) pipe carries seal groove.
The utility model produce beneficial effect be:
The membrane component of proposition of the present utility model, the water inlet flow channel cloth of only diversion function and production water flow passage cloth are replaced with
Runner cloth with scale inhibition and sorbing material, the central tube for only collecting production water function is become there is improvement mouthfeel and sterilization to make
With, and diaphragm also has retention and adsorption function.Membrane component with scale inhibition, filtering and adsorption function, does not increase volume increasing
Function is added, producing water water quality is more preferable, and the membrane component gathered multi -function in integral whole can simplify water purification group technology, reduces water purification
Cost, is more favorable for promoting the use of for water purification product.
Brief description of the drawings
In order to be easier to understand the technical solution of the utility model and beneficial technique effect, by referring to showing in the accompanying drawings
The utility model is described in detail for the embodiment of the present utility model that goes out.These accompanying drawings depict only this reality
With new exemplary embodiment, the limitation to protection domain of the present utility model is not constituted, wherein:
Fig. 1 is the knot of the membrane component of the simplification water-purifying process with a variety of functions according to embodiment of the present utility model
Structure schematic diagram.
In the reference indicated in Fig. 1:
1:Diaphragm;2:Produce water flow passage cloth;3:Water inlet flow channel cloth;4:Sealing;5:Produce water end (W.E.) pipe;6:Produce water end (W.E.) seal of tube groove;
7:Collector pipe;8:Water inlet end pipe dividing plate;9:Water inlet end pipe.
Embodiment
A kind of membrane component of simplification water-purifying process with a variety of functions as shown in Figure 1, it mainly includes diaphragm 1, production
Water flow passage cloth 2, water inlet flow channel cloth 3 and central tube, production water flow passage cloth 2, the diaphragm 1 folded, the feed water flow being clipped in folding diaphragm 1
Road cloth 3 is sequentially stacked together volume according to this on central tube, water inlet flow channel cloth 3 and the composition intake tunnel of diaphragm 1, produces water flow passage
Composition production aquaporin after cloth 2 and diaphragm 1 are bonded, production water is collected by central tube.
Diaphragm 1 has filtering and adsorption function, and described diaphragm includes the selectivity such as micro-filtration, ultrafiltration, nanofiltration and counter-infiltration
Through diaphragm, homogeneous diaphragm load or grafting sorbing material can reach adsorption effect in retention layer, and heterogeneous diaphragm can be in branch
Load or grafting sorbing material reach adsorption effect in support layer.
Water inlet end pipe 9, collector pipe 7 and production water end (W.E.) pipe 5 that central tube includes.Water inlet end pipe and water inlet are communicated, to make into water
Separated with production water, water inlet end pipe dividing plate 8 is set in water inlet end pipe 9.Central tube interlude is collector pipe 7, collects production water flow passage cloth 2
The production water that water conservancy diversion comes, what is be connected with collector pipe 7 is production water end (W.E.) pipe 5, to prevent waste water from entering central tube, in production water end (W.E.) pipe 5
On have production water end (W.E.) seal of tube groove 6.
As shown in figure 1, diaphragm 1 and the both sides vertical with central tube of production water flow passage cloth 2 and parallel with central tube and remote center
Pipe all uses the edge sealing of sealing 4 on one side.
Water inlet constitutes intake tunnel by diaphragm 1 and water inlet flow channel cloth 3 and enters membrane component, and water inlet flow channel cloth 3 makes equal into water
It is even to be distributed in film surface, while the nano controlled-release capsule being supported on water inlet flow channel cloth discharges the sustained release scale inhibition factor into water inlet,
Obstruction forms inorganic scale polluted membrane surface, increases the stain resistance of element, has in the absorption water inlet of water inlet flow channel cloth 3 to diaphragm broken
The material increase component life of bad property.
In addition, described water inlet flow channel cloth 3 can also may be used by the directly machine-shaping of sorbing material such as resin, Carbon fibe etc.
Sorbing material is loaded on water inlet flow channel cloth 3 or by methods such as modified grafting with adsorption function, in water inlet flow channel cloth 3
There is the sustained release factor of scale inhibition function in upper grafting or load, scale inhibition effect is reached.Described production water flow passage cloth 2, which has, leads
Miscarriage water is to central tube and adsorbs harmful substance that diaphragm can not be retained or that rejection is low.Described production water flow passage cloth 2 can be with
By the directly machine-shaping of sorbing material such as resin, Carbon fibe etc., sorbing material can be also loaded on production water flow passage cloth 2 or by changing
Property grafting etc. method with adsorption function.
Water inlet is in the presence of driving force, and through the selective pellicle as the diaphragm 1, water inlet is now transmitted through semi-transparent
During film, in addition to retention layer is retained to polluter, nanocarbon particle in diaphragm is supported on, residual substance is adsorbed,
Water entrance diaphragm 1 and the production composition production aquaporin of water flow passage 2 are produced, the production water flow passage cloth 2 made by activated carbon fiber material will produced
While water water conservancy diversion is to central tube, the material that 2 pairs of production water flow passage cloth is produced can not retain in water or rejection is low is further adsorbed, and is produced
Water flow passage cloth 2 is longer because of flow, and adsorption effect is more preferable.
Production water reaches central tube and entered by the micropore on sintering activity charcoal collector pipe 7 in central tube.Production water passes through
During micropore, the sense of the production mouth of a river is improved, while the Nano Silver being supported on collector pipe 7, which can also kill bacterium, ensures production water security.
Production water is flowed out by producing water end (W.E.) pipe 5.The central tube has absorption and sterilizing function.The water inlet end pipe 9 is waterproof densification
Material, the collector pipe 7 is made up of the sorbing material with sterilizing function, and with a large amount of micropore aquaporins, the production water end (W.E.)
Pipe 5 is waterproof dense material.
Embodiment of the present utility model is explained above in association with accompanying drawing, active carbon adsorption material herein
It is only a kind of embodiment of the present utility model with bactericidal nano-silver material, but protection domain of the present utility model not office
It is limited to this, it is any to depart from change or replacement of the present utility model without essence, also it is all contained in protection domain of the present utility model
Within.Protection domain of the present utility model is defined only by the following claims.
Claims (6)
1. a kind of membrane component of the simplification water-purifying process with a variety of functions, including diaphragm, production water flow passage cloth, water inlet flow channel cloth and
Central tube, production water flow passage cloth, the diaphragm folded, is clipped in the water inlet flow channel cloth folded in diaphragm and is sequentially stacked together according to this volume
On central tube, water inlet flow channel cloth and diaphragm composition intake tunnel produce composition production aquaporin, production after water flow passage cloth and diaphragm bonding
Water is collected by central tube, the central tube by water inlet end pipe, collector pipe and production water end (W.E.) pipe constitute, it is described water inlet end pipe on have into
Water dividing plate, diaphragm and production water flow passage cloth both sides vertical with central tube and parallel with central tube and remote central tube all use sealing on one side
Edge sealing.
2. membrane component according to claim 1, wherein described water inlet flow channel cloth and/or described production water flow passage cloth are by inhaling
The direct machine-shaping of enclosure material is loading sorbing material or by modified grafting method with adsorption function thereon.
3. membrane component according to claim 1, wherein described diaphragm includes micro-filtration, ultrafiltration, nanofiltration and counter-infiltration selection
Property pass through diaphragm, homogeneous diaphragm load or grafting sorbing material in retention layer, heterogeneous diaphragm are loaded or connect in supporting layer
Branch sorbing material.
4. the membrane component according to any one of claim 1-3, wherein the water inlet end pipe and production water end (W.E.) pipe are waterproof
Dense material.
5. the membrane component according to any one of claim 1-3, wherein the collector pipe is by the absorption with sterilizing function
Material is constituted and with a large amount of micropore aquaporins.
6. the membrane component according to any one of claim 1-3, wherein the production water end (W.E.) pipe carries seal groove.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110975618A (en) * | 2019-11-18 | 2020-04-10 | 厦门百霖净水科技有限公司 | A roll film structure |
CN111111455A (en) * | 2020-01-11 | 2020-05-08 | 苏州曙之洁环保科技有限公司 | Composite reverse osmosis membrane assembly |
CN111185102A (en) * | 2019-08-02 | 2020-05-22 | 珠海格力电器股份有限公司 | Spiral wound membrane module and water purification system |
CN115463549A (en) * | 2022-08-25 | 2022-12-13 | 万华化学集团股份有限公司 | Preparation method and application of membrane element water inlet runner net resistant to biological pollution |
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2017
- 2017-01-17 CN CN201720049882.XU patent/CN206463797U/en active Active
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CN111185102A (en) * | 2019-08-02 | 2020-05-22 | 珠海格力电器股份有限公司 | Spiral wound membrane module and water purification system |
CN111185101A (en) * | 2019-08-02 | 2020-05-22 | 珠海格力电器股份有限公司 | Water purification unit with filter element group spare |
CN111185096A (en) * | 2019-08-02 | 2020-05-22 | 珠海格力电器股份有限公司 | Compound filter element group spare and water purification system |
CN111185100A (en) * | 2019-08-02 | 2020-05-22 | 珠海格力电器股份有限公司 | Central tube for roll type membrane, roll type membrane component and water purification system |
CN111229057A (en) * | 2019-08-02 | 2020-06-05 | 珠海格力电器股份有限公司 | A composite filter element assembly and water purification system |
CN111229054A (en) * | 2019-08-02 | 2020-06-05 | 珠海格力电器股份有限公司 | A composite filter element assembly and water purification system |
CN111229056A (en) * | 2019-08-02 | 2020-06-05 | 珠海格力电器股份有限公司 | Compound filter element group spare and water purification system |
CN111229055A (en) * | 2019-08-02 | 2020-06-05 | 珠海格力电器股份有限公司 | A composite filter element assembly and water purification system |
CN111318175A (en) * | 2019-08-02 | 2020-06-23 | 珠海格力电器股份有限公司 | Spiral wound membrane module and water purification system |
CN110975618A (en) * | 2019-11-18 | 2020-04-10 | 厦门百霖净水科技有限公司 | A roll film structure |
CN111111455A (en) * | 2020-01-11 | 2020-05-08 | 苏州曙之洁环保科技有限公司 | Composite reverse osmosis membrane assembly |
CN115463549A (en) * | 2022-08-25 | 2022-12-13 | 万华化学集团股份有限公司 | Preparation method and application of membrane element water inlet runner net resistant to biological pollution |
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